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이보성,유승곤,김혜영,Rhee Bo Sung,Ryu Seung Kon,Kim Hae Yeong Korean Chemical Society 1978 대한화학회지 Vol.22 No.5
化學反應 수반하는 氣體吸着反應器의 設計에 가장 重要한 氣液界面間의 物質傳達係數와 面積을 測定하는데 자주 모델反應이 利用된다. 本硏究는 그 中에서 wetted wall column 에 sulfite-system을 dldydgkdu 特別히 氣液間의 接觸時間이 氣體吸着速道에 미치는 영향을 硏究 檢討하였다. 反應速道가 매우 빠르거나 늦으면 column의 길이에 따라서, 다시 말하면 接觸時間에 따라서 氣體吸着速道에 差異가 크다는 것을 發見했다. 反應速道恒數 $k_2=5.5{\times}10^6m^3/kmol{\cdot}s$ 近處에서는 이 差異가 없어진다. 換言하면 이런 條件下에서 裝置의 hydrodynamics가 氣體吸着速道에 無關해진다. 金屬 column 代身에 graphite column을 使用할 수 있다는 例證을 題示하였다. Model reactions were often applied in the measuring of the mass transfer coefficient and interfacial area between gas and liquid, which are the most important factors in the design of equipment for gas absorption accompanied with chemical reaction this study, wetted wall column was applied to the sulfite-system among the known model reactions. It was found that one could not ignore the effect of contact time on the determination of mass transfer coefficient and interfacial area. When the reaction rate is very high or very low, the differences of absorption rate would be very large in according to the length of column, that is to the contact time. But the effect of contact time was free about the rate constant $k_2=5.5{\times}10^6m^3/kmol{\cdot}s$, that means the rate of gas absorption become independent upon the hydrodynamics of the equipment. It has shown that instead of steel column could be applied the fine grain-graphite column.
경막 결정화기에서 벤젠 - 시클로헥산 혼합물로부터 벤젠의 결정성장속도
김광주,이정민,유승곤 ( Kwang Joo Kim,Jung Min Lee,Seung Kon Ryu ) 한국공업화학회 1996 공업화학 Vol.7 No.2
경막형 결정화기에서 벤젠-시클로헥산 혼합물로부터 벤젠의 결정성장속도가 조사되었다. 결정성장속도는 경막결정화기의 냉각벽에 부착되는 결정의 양으로부터 얻어진 결정두께와 시간에 대한 상관관계식으로부터 결정되었다. 결정 성장속도와 결정의 표면온도와, 용융액의 온도의 차로 정의되는 과냉각정도와의 상관관계가 얻어졌다. 이 이성분 공융계에 대한 결정성장속도는 과냉각정도의 2승에 비례하였다. 경막결정화기의 열전달 및 물질전달 속도에 근거하여 결정의 표면온도 및 결정두께를 예측할 수 있는 모델식이 제시되었다. 5wt% 및 10wt%의 시클로헥산을 포함한 벤젠-시클로헥산 혼합물에 대하여 여러 다른 냉각온도에서 실험적으로 얻어진 결정두께의 자료와 모델식으로 계산된 결과가 비교되었다. The crystal growth rate of benzene from benzene-cyclohexane mixtures at a cylindrical layer crystallizer was determined from the slope of the line of correlation between operating time and layer thickness. The thickness of crystal layer was obtained from the amount of crystal deposited on the cooled wall surface of the crystallizes. The crystal growth rate was related with the degree of subcooling, which was defined as the difference between temperature of melt and that of growing crystal surface. The linear crystal growth rate for binary mixtures was proportional to the second power of the degree of subcooling. Equation model which was obtained from data through the rate of heat and mass transfer in the crystallizes and thus can tell crystal thickness and surface temperature of crystal layer according to the elapsed time was presented and successfully correlated to the experimental data. For the benzene-cyclohexane mixtures containg 5wt% and 10wt% of cyclohexane, the comparison of experimental data with calculation using model equation was done for crystal thickness corresponding to the various cooling temperatures.